|Numéro de publication||US5054556 A|
|Type de publication||Octroi|
|Numéro de demande||US 07/524,433|
|Date de publication||8 oct. 1991|
|Date de dépôt||17 mai 1990|
|Date de priorité||17 mai 1990|
|État de paiement des frais||Payé|
|Numéro de publication||07524433, 524433, US 5054556 A, US 5054556A, US-A-5054556, US5054556 A, US5054556A|
|Inventeurs||Yeshayahu Greitzer, Lucient Y. Bronicki|
|Cessionnaire d'origine||Ormat Turbines (1965) Ltd.|
|Exporter la citation||BiBTeX, EndNote, RefMan|
|Citations de brevets (10), Référencé par (5), Classifications (18), Événements juridiques (8)|
|Liens externes: USPTO, Cession USPTO, Espacenet|
1. Technical Field
This invention relates to a method of and for operating a geothermal well, and more particularly, for increasing its flow rate.
2. Background Art
As a geothermal field ages by reason of long term extraction of hot geothermal fluid from geological formations in the field, and long term reinjection of spent heat depleted geothermal fluid into the field, two results often occur: 1) a reduction in the mass flow rate and temperature of hot geothermal fluid from production wells in the field; and 2) an increase in the pressure required to reinject spent geothermal fluid into injection wells in the field. Both problems apparently result from reductions in the permeability of the geological formations in the field.
Another common problem that often occurs in an operating geothermal field is coupling between an injection well and a production well whereby the heat depleted geothermal fluid pumped into the injection well begins to adversely affect the temperature of the hot geothermal fluid extracted from a nearby production well. The exact mechanism that controls these results is not entirely understood at this time, but it is presently believed that the problems are related to the permeability, or changes in the permeability, of the geological formations in which the wells are located. Such changes apparently are caused by long-term extraction of hot geothermal fluid from, and long-term injection of spent geothermal fluid into, the geological formations of a field.
In order to increase the rate at which spent geothermal fluid can be disposed of in an injection well, it is conventional to carry out what is termed "acidizing" the well. Such approach is also used for increasing the flow rate of geothermal fluid from a production well. This is a procedure by which concentrated acid is applied to a stratum whose location and nature is determined from geological studies for the purpose of increasing the permeability of the stratum by the dissolving action of the acid on the rock in the stratum. The procedure, which is time consuming, costly, and dangerous, requires the injection well to be taken out of operation.
The first step after operation is terminated is to place rubber seals in the well at the upper and lower limits of the stratum to be treated. These placements require the use of a rig having drilling pipes for inserting and withdrawing the rubber seals; and usually, a considerable investment in time and labor is involved. Next, a pipe is run down the well from the surface to the upper seal for gaining access to the region of the well between the rubber seals. An acid solution of 10-20% concentration is then pumped through the pipe into the volume between the seals for a period of from 1 to a few hours. Both water and acid must be trucked to the well-head for this purpose; and a considerable volume of liquid is required for this operation. The acid solution percolates through the stratum defined by the seals and dissolves some of the rock therein increasing the permeability of the stratum. Finally, the rubber seals are removed by the rig, and operation can be resumed.
This is a batch approach to increasing the permeability of a stratum. It is expensive because the well being treated must be taken out of operation, and testing of the efficacy of the treatment can be done only by closing the well and resuming operations. This results in a tendency to over-treat a well which further increases the cost in money and time.
Concerning the problem of leakage between an injection well and a production well, no practical solution is presently available. All of these problems are beginning to seriously affect existing geothermal fields which still contain a significant amount of energy extraction is highly desirable.
It is therefore an object of the present invention to provide a new and improved method of and means for operating geothermal wells to selectively modify the permeability of geological formations in which both injection and production wells are located.
According to the present invention, spent geothermal fluid is continuously applied to a geothermal well, using a pump, for example, and sufficient concentrated acid is continuously added to the spent geothermal fluid such that the concentration of acid in the fluid is in the range 0.5% to 10%, but preferably, that concentration is not greater than 5%. Normally, this operation will occur over a period of time measured in days or weeks, rather than hours as in the case of the prior art, and is thus a continuous rather than a batch process. The geothermal fluid referred to in this specification is mostly geothermal liquid. Even so, the term should be taken to include steam, wherein the steam may be present with liquid, or steam alone. Preferably, some quantities of substances such as inhibitors suitable for reducing corrosive effects of the acid solution on the well casing or liner may be added to the spent geothermal fluid, particularly to control the pH of the dilute acid solution. Usually, the pH will be increased by the additives.
In accordance with the invention, the natural flow of the geothermal fluid through the various strata of the geological formation in which the well is located, will carry the dilute acid to those portions of the formation susceptible to being dissolved. The integrated effect of the exposure of the rock in the formation to dilute acid over a relatively long period of time is to slowly increase the permeability of the various strata throughout the entire field in which the spent geothermal fluid flows. This continuous process, which is from the batch process of the prior art, does not require suspension of operation of an injection well, and ensures the application of an acid solution to whatever strata the flow of spent fluid passes, thereby applying the dilute acid to the various strata. The long term effect of this approach is to increase the permeability of various strata thereby decreasing the resistance of the injection well to the flow of spent geothermal fluid.
The acid solution may be added to the spent geothermal fluid before the latter enters the well. Preferably, however, the acid solution is added to the fluid at a predetermined depth in the well consistent with the location of the slotted liner in the well through which the geothermal fluid flows into the surrounding rock formations. This latter operation is carried out by inserting a conduit into the injection well such that the lower end of the conduit is located below the upper unslotted metallic casing of the well. This has the advantage of protecting the upper casing from being corroded by the dilute acid. A solution of concentrated acid is then pumped into the upper end of the conduit so that the solution exits the lower end below the casing and is carried by the spent geothermal fluid into the geothermal formations in which the well is located.
The present invention also involves a method for increasing flow from a production well. In such case, the flow of hot geothermal fluid from the production well is terminated, and spent geothermal fluid is diverted from a nearby injection well and forced into the production well. Acid solution is added to the spent geothermal fluid in the manner described above, preferably by piping the dilute acid to a level below the unperforated casing. Over a period of several days or weeks, the dilute acid will increase the permeability of the rock formations penetrated by the spent geothermal fluid carrying the dilute acid. At the end of the treatment period, production of the well may be resumed with an increased rate of flow.
The present invention also involves a method for reducing leakage between an injection well that receives spent geothermal fluid, and a production well that produces high temperature geothermal fluid. According to the present invention, a conduit is inserted into the injection well to a depth consistent with the stratum in which leakage is believed to occur between the injection well and the production well. Components of drilling mud, or other material suitable for reducing the permeability of the stratum can be pumped into the conduit for effecting a flow of the mud or other material into the stratum: reducing its permeability and suppressing further leakage. Alternatively, drilling mud components, or other suitable material, can be added to the spent geothermal fluid before it enters the well. In such case, the mud or other material flows with the spent geothermal fluid as the latter flows along its usual paths into the stratum surrounding the well locally reducing its permeability, thus reducing the underground fluid flow velocity, and suppressing further leakage. Furthermore, such methods can be used to merely reduce permeability of certain formation strata surrounding the well.
In addition, the present invention also involves a method for developing a new geothermal injection or production well once drilling is completed. According to the present invention, preferably spent geothermal fluid form a nearby injection well is diverted to the drilled well and forced into the well. Acid solution is added, in the manner described above, to the geothermal fluid for the purpose of increasing the permeability of rock formations surrounding the well. At the end of the treatment period, operation of the well as an injection or production well, as the case may be, can be commenced.
Embodiments of the present invention are shown by way of example in the accompanying drawings wherein:
FIG. 1 is a schematic block diagram showing one aspect of the present invention wherein acid solution is continuously added to the spent geothermal fluid being injected into a well in a geothermal field;
FIG. 2 is a schematic block diagram showing another embodiment of the present invention for treating an injection well or a production well with dilute acid in a continuous process;
FIG. 3 is a further embodiment of the present invention;
FIG. 4 is a still further embodiment of the present invention for reducing leakage between an injection well and a production well; and
FIG. 4A is another embodiment of the present invention for reducing leakage between an injection well and a production well.
Referring now to FIG. 1 of the drawings, reference numeral 10 designates apparatus according to the present invention for adding concentrated acid to spent geothermal fluid that is pumped into a rejection well. That is to say, source 12 represents the equipment that operates on hot geothermal fluid, extracts heat therefrom, and produces spent, or heat depleted geothermal fluid that must be disposed of. Pump 14 may be provided for pressurizes the spent fluid before the latter is delivered to well-head 16 via pipe 18. Such fluid is applied to injection well 20, and the pressure is sufficient to force the fluid down the well and through the openings in slotted liner 22 that constitutes the lower portion of the well. The fluid that exits the well enters into and flows through permeable rock in the geological formation in which the well is located until the pressure is dissipated.
As the well ages, the permeability of the rock formations apparently decrease, perhaps due to the precipitation of the mineral rich fluid which is cooled by contact with the rock formations. Furthermore, it could well be that the permeability of the rock formations surrounding the well was initially insufficient. In any event, experience has shown that injection pressure must be increased with time to maintain the same mass flow of fluid. The first approach to ameliorating this problem is shown in FIG. 1 wherein concentrated acid, preferably hydrochloric acid, in source 24 is metered at 26 into the flow of fluid in pipe 18 such that the concentration of acid in the fluid is in the range 0.5% to 10%. Preferably, the concentration does not exceed about 5%. Small quantities of additives, such as inhibitors present in container 25, are fed into the spent geothermal fluid to reduce corrosive action of the acid solution on the well casing or lining by controlling the pH of the diluted acid.
As a consequence, the spent geothermal fluid carrying the dilute acid flows through slotted liner 22 along its usual paths into the rock formation surrounding the well. Wherever dissolvable rock is encountered in these paths, the dilute acid reacts with the rock increasing its permeability.
The treatment continues over a period of time measured in days and weeks as the dilute acid slowly but effectively continues to dissolve rock in the flow path of the fluid. The effect on the surrounding rock formations is the integration over a long period of time of dilute acid acting on the rock; and eventually, the permeability of the rock will be sufficiently increased to result in a reduction in the pressure needed in order to dispose of the spent geothermal fluid.
The actual amount of time will, of course, depend on the nature of the geological formation in which the well is located; but it is presently contemplated that a time period in excess of 24 hours will be required, and probably of the order of magnitude of a week. In this sense, therefore, the present invention involves a continuous treatment of the entire well without interrupting its operation, as distinguished from the conventional treatment which is a batch process that involves shutting down the well and acidizing only a preselected stratum for only a few hours.
Because the dilute acid in the spent geothermal fluid may have a corrosive effect on the well head equipment and the upper casing of the well above the lower slotted liner 22A, the arrangement shown in FIG. 2 is preferred when the concentration of acid in the fluid exceeds about 1%. As shown in FIG. 2, well 20A is treated, according to the present invention, by metering concentrated acid into the spent geothermal fluid at a location below casing structure 28 of the well. To effect this operation, conduit 29 is inserted into the well to a depth consistent with the location at which acid treatment is to begin. This depth is determined by an analysis of geological information associated with the well which is beyond the scope of this specification, suffice it to say that conduit 29 is inserted into the well, preferably such that its lower end 30 is located at the desired depth, and its upper end 31 terminates in a connection to source 24A.
Metering pump 32 pumps concentrated acid from source 24A to lower end 30 of the conduit into the well at a rate such that the concentration of acid in the spent geothermal fluid at the outlet of the conduit no greater than about 10%, but preferably no greater than about 5%. The treatment region will be that portion of the geological field affected by the flow of fluid from the well below the end 30 of the conduit.
A further embodiment of the invention is shown in FIG. 3 wherein two reactants are injected into the geothermal fluid, the reactants producing a reaction product when they mix. In a manner analogous to the operation of the embodiments described above, the flow of geothermal fluid into the geological formation surrounding the well serves to carry the product into the rock formations for changing the permeability of thereof. Depending upon the nature of the product, the permeability may be increased or decreased.
Specifically, geothermal fluid is pumped down well 20B in the usual manner; but, as shown in FIG. 3, conduit 31B extends from the surface of the well to a level below casing 28B in the vicinity of the upper portion of slotted liner 22B. Conduit 31B comprises a pair of pipes 32, 33 whose top ends 34, 35 are connected respectively to different reactant sources 36, 37. The reactants in the sources are of the type that react to form a reaction product when mixed.
In operation, conduit 31B is inserted into the well, and metering pumps 38 inject the two reactants into the well at the level determined by the lower end of the conduit. The two reactants mix together when they exit from pipes 32, 33 producing a product that is carried by the flowing geothermal fluid into the surrounding rock formation. As before, the time period over which the product is produced is measured in days and weeks, depending on the nature of the product.
Furthermore, the present invention also contemplates injecting components of drilling mud or other suitable materials into an operating injection well for the purpose of decoupling the well from a production well. This approach is illustrated in FIG. 4 where conduit 31C is located in injection well 20C which is in the vicinity of production well 40 from which hot geothermal fluid is withdrawn. The lower end of the conduit is located at a level consistent with a leakage path 41 that connects well 20C to well 40. Components of drilling mud, produced at the surface of the injection well, are pumped into the injection well through conduit 31C and flow though the slotted liner into the rock formation following the path of least resistance which is the leakage coupling to the production well. The result is that the drilling mud components, or other material decrease the local permeability of the rock formations through which they percolate, reducing underground fluid flow velocity and achieving decoupling the injection well from the production well. If preferred, decoupling of an injection well from a production well also can be achieved using an arrangement similar to that illustrated in FIG. 1. As shown in FIG. 4A, components of drilling mud, or other suitable materials, present in container 24D can be added to spent geothermal fluid flowing in pipe 18D prior to the entry of the fluid into the injection well. Furthermore, such method can be used merely to reduce permeability of certain formation strata surrounding the well.
Additionally, the present invention also can be used for developing new geothermal injection or production wells once drilling is completed. Methods shown in FIGS. 1-3 can be used for adding acid solutions, or other suitable chemicals, to spent geothermal fluid diverted from an injection well and forced into the newly drilled well. The fluid carrying the dilute acid will flow into rock formations surrounding the well, and the dilute acid will react with the formations increasing their permeability. Subsequently, at the end of the treatment period, operation of the well as an injection or production well, as the case may be, can be commenced.
At present, it is envisaged that the present invention will be carried out to change the permeability of rock formations at depths ranging from 100-2000 m. However, in actual fact, the invention can be used for changing the permeability of rock formations at any depth.
The advantages and improved results furnished by the method and apparatus of the present invention are apparent from the foregoing description of the preferred embodiment of the invention. Various changes and modifications may be made without departing from the spirit and scope of the invention as described in the appended claims.
|Brevet cité||Date de dépôt||Date de publication||Déposant||Titre|
|US2761511 *||23 mars 1953||4 sept. 1956||Billue Gaines H||Treatment of earth formations|
|US3111006 *||7 juin 1960||19 nov. 1963||Soletanche||Novel method for injecting clay-containing grout into ground and products serving for the execution of said method|
|US4059156 *||29 avr. 1976||22 nov. 1977||Berg Clyde H||Geothermal brine production|
|US4093310 *||19 sept. 1977||6 juin 1978||In Situ Technology, Inc.||Sealing an underground coal deposit for in situ production|
|US4476930 *||23 août 1982||16 oct. 1984||Union Oil Company Of California||Inhibition of scale deposition from steam generation fluids|
|US4500434 *||2 déc. 1982||19 févr. 1985||Union Oil Company Of California||Inhibiting scale precipitation from high temperature brine|
|US4507925 *||7 mai 1981||2 avr. 1985||Schaetzle Walter J||Method for and thermal energy injection withdrawal system for aquifers|
|US4542625 *||20 juil. 1984||24 sept. 1985||Bronicki Lucien Y||Geothermal power plant and method for operating the same|
|US4632601 *||1 nov. 1985||30 déc. 1986||Kuwada James T||System and method for disposal of noncondensable gases from geothermal wells|
|US4830766 *||15 oct. 1986||16 mai 1989||Union Oil Company Of California||Use of reducing agents to control scale deposition from high temperature brine|
|Brevet citant||Date de dépôt||Date de publication||Déposant||Titre|
|US5372194 *||10 mai 1993||13 déc. 1994||Ormat Turbines (1965) Ltd.||Method of and means for operating geothermal wells|
|US5979556 *||25 juil. 1996||9 nov. 1999||Union Oil Company Of California||Slow acidizing of geological formations|
|CN100545545C||18 juin 2008||30 sept. 2009||刘娇娜||Ground water back pouring cyclic utilization method|
|CN102720488A *||11 juil. 2012||10 oct. 2012||西南石油大学||Testing device and method for simulating flat carbonate rock reaction|
|CN102720488B||11 juil. 2012||22 oct. 2014||西南石油大学||用模拟平板酸岩反应的测试装置模拟平板酸岩反应的方法|
|Classification aux États-Unis||166/302, 166/57, 166/307, 60/641.5, 166/292|
|Classification internationale||E21B33/138, C09K8/72, F24J3/08, E21B43/26|
|Classification coopérative||E21B43/26, Y02E10/14, F24J3/085, C09K8/72, E21B33/138|
|Classification européenne||E21B33/138, F24J3/08B, C09K8/72, E21B43/26|
|8 mars 1991||AS||Assignment|
Owner name: ORMAT TURBINES (1965) LTD., A CORP. OF ISRAEL, ISR
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:GREITZER, YESHAYAHU;BRONICKI, LUCIEN Y.;REEL/FRAME:005623/0841
Effective date: 19910207
|28 mars 1995||FPAY||Fee payment|
Year of fee payment: 4
|7 avr. 1999||FPAY||Fee payment|
Year of fee payment: 8
|19 avr. 2001||AS||Assignment|
Owner name: ORMAT INDUSTRIES LTD., ISRAEL
Free format text: CHANGE OF NAME;ASSIGNOR:ORMAT TURBINES (1965) LTD.;REEL/FRAME:011722/0236
Effective date: 19920917
|23 avr. 2003||REMI||Maintenance fee reminder mailed|
|2 oct. 2003||SULP||Surcharge for late payment|
Year of fee payment: 11
|2 oct. 2003||FPAY||Fee payment|
Year of fee payment: 12
|6 janv. 2005||AS||Assignment|
Owner name: ORMAT TECHNOLOGIES, INC., NEVADA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:ORMAT INDUSTRIES, LTD;REEL/FRAME:015541/0547
Effective date: 20050106